Classifications

• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
  • C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
  • C07C1/24—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms by elimination of water
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
  • C07C41/01—Preparation of ethers
  • C07C41/09—Preparation of ethers by dehydration of compounds containing hydroxy groups
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
• • E—FIXED CONSTRUCTIONS
  • E21—EARTH OR ROCK DRILLING; MINING
  • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
  • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
  • E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
  • E21B43/164—Injecting CO2 or carbonated water
• • E—FIXED CONSTRUCTIONS
  • E21—EARTH OR ROCK DRILLING; MINING
  • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
  • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
  • E21B43/25—Methods for stimulating production
  • E21B43/26—Methods for stimulating production by forming crevices or fractures
• • E—FIXED CONSTRUCTIONS
  • E21—EARTH OR ROCK DRILLING; MINING
  • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
  • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
  • E21B43/25—Methods for stimulating production
  • E21B43/26—Methods for stimulating production by forming crevices or fractures
  • E21B43/2605—Methods for stimulating production by forming crevices or fractures using gas or liquefied gas
• • E—FIXED CONSTRUCTIONS
  • E21—EARTH OR ROCK DRILLING; MINING
  • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
  • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
  • E21B43/25—Methods for stimulating production
  • E21B43/26—Methods for stimulating production by forming crevices or fractures
  • E21B43/267—Methods for stimulating production by forming crevices or fractures reinforcing fractures by propping
• • E—FIXED CONSTRUCTIONS
  • E21—EARTH OR ROCK DRILLING; MINING
  • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
  • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
  • E21B43/34—Arrangements for separating materials produced by the well
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
  • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
  • C10L2290/42—Fischer-Tropsch steps
• • E—FIXED CONSTRUCTIONS
  • E21—EARTH OR ROCK DRILLING; MINING
  • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
  • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
  • E21B43/34—Arrangements for separating materials produced by the well
  • E21B43/40—Separation associated with re-injection of separated materials
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P90/00—Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
  • Y02P90/70—Combining sequestration of CO2 and exploitation of hydrocarbons by injecting CO2 or carbonated water in oil wells

Definitions

• US patent application publication 2013/0056205 discloses the use of argon as a supercritical fluid and proppant for fracking, but this involves use of a gel, foaming agent or other gas for successful delivery to the subterraneum formation.
• US patent application publication 2012/0118566 suggests pumping metacritical phase natural gas to create or extend one or more fissures in a subterraneum formation for fracking. This is disclosed as being an improvement over hydraulic fracturing methods that use water, liquid nitrogen or liquid carbon dioxide, the latter of which is disclosed as requiring foaming agents. Furthermore, the used carbon dioxide would be released to the atmosphere where it can contribute to global warming or other harmful environmental conditions.
• US patent application publication 2007/0261844 discloses a closed loop system for the capture and sequestering of carbon dioxide associated with the extraction of energy sources from large land masses. It suggests sequestering carbon dioxide in a shale reservoir or other formation. Sequestering of carbon dioxide, however, is not a viable solution for preventing the emission of carbon dioxide into the atmosphere, since the sequestration does not assure that the carbon dioxide will be maintained in the ground. The same is true of other forms of sequestration such as under the sea or in underground caverns.
• CO 2 injection into depleting oil fields and gas wells is used to improve secondary oil and gas recovery.
• the use of CO 2 gas for fracking shale has not been utilized commercially and has been explored on a limited scale only. This technology was considered economically and technically impractical (see, e.g., K. Bullis, MIT Technology Review, Mar. 28, 2013).
• the present invention avoids hydraulic fracking, as well as emitting carbon dioxide into the atmosphere while producing methanol providing an alternative general transportation fuel and chemical source material. It is thus a highly valuable process for replacing petroleum oil.
• the invention relates to a method of producing methanol by obtaining shale gas and by using dry CO 2 fracking.
• the method involves dry fracking of shale rock by injection of gaseous CO 2 at a pressure of 10 to 100 atm to extract shale gas from its rock formations.
• the recovered shale gas is subsequently cleaned to remove contaminants including hydrogen sulfide and provide a clean shale gas comprising essentially methane and some of its homologues.
• Further steps include subsequent combining of the cleaned shale gas with CO 2 and water (steam) to produce a mixture of methane:carbon dioxide:water at a molar ratio of 3:1:2; conducting the bi-reforming reaction to form exclusively a mixture of hydrogen and carbon monoxide having a molar ratio of 2:1 to 2.1:1; and subsequently converting this mixture (metgas) under conditions sufficient to exclusively form methanol.
• CO 2 from any available source is used for dry fracturing (fracking) of the natural gas containing shale formation.
• CO 2 is also separated from the liberated shale gas (methane) to provide CO 2 to be recycled to the injection step while part of the separated or accompanying CO 2 together with the needed amount of water (typically as steam) is used for the subsequent bireforming step.
• Injection CO 2 is produced from any natural or unnatural (industrial) source and is pressurized to the desired pressure of between 10 and 100 atm prior to injection into the shale rock.
• Energy needed for the bi-reforming reaction may be provided from any available energy source, including combustion of part of the methane from the recovered shale gas or from one or more alternative or green sources of energy.
• the bi-reforming reactions are carried out over a catalyst at a temperature between about 800° C. and 1100° C. and a pressure of 5 to 40 atm, wherein the catalyst comprises V, Ti, Ga, Mg, Cu, Ni, Mo, Bi, Fe, Mn, Co, Nb, Zr, La or Sn, or oxides thereof in the form of a single metal catalyst, a single metal oxide catalyst, a mixed catalyst of a metal and a metal oxide, or a mixed catalyst of at least one metal oxide and another metal oxide, the catalyst optionally being provided on an oxide support.
• the produced metgas is directly converted to methanol.
• the method can further comprise dehydrating all or a portion of the methanol to dimethyl ether (DME) and recycling the water from the dehydration step to the bi-reforming reaction.
• DME dimethyl ether
• all or part of the dimethyl ether can be converted in the presence of a bifunctional (an acid-base) or zeolite catalyst under sufficient conditions to form ethylene and/or propylene.
• the ethylene and/or propylene can be further converted under conditions sufficient to higher olefins, synthetic hydrocarbons, aromatics, or products produced therefrom, for use as a feedstock for chemicals or transportation fuels.
• the invention also relates to various uses of the methanol that is formed from the methods disclosed herein.
• the methanol can be used as an essential economic and replenishable energy source material for conversion to hydrocarbon fuels, dimethyl ether or products derived from dimethyl ether.
• Methanol can also be used as a commonly useful fuel for internal combustion engines by admixing the methanol to or replacing gasoline or diesel fuel with methanol for combustion in modified or adjusted internal combustion engines.
• the present invention avoids the problems inherent with hydraulic fracking with water while also avoiding carbon dioxide emission into the atmosphere. Furthermore, an alternative energy fuel is provided by the present processes. These beneficial and unexpected advantages are achieved by utilizing shale gas containing CO 2 as a feed-stock to synthesize metgas (2H 2 :CO) for methanol synthesis through the process of bireforming.
• the present invention eliminates the use of hydrofracking with all its disadvantages and harm replacing it with “dry fracking” using CO 2 . It involves the injection of pressurized CO 2 from any source through the borehole into the shale formations and recovering freed shale gas (methane) as well as using it together with CO 2 used for fracking. Part of the recovered CO 2 together with needed amount of steam is used for subsequent bireforming for metgas and thus methanol synthesis.
• This is the specific advantage of the presently disclosed dry fracking with CO 2 involving subsequent shale gas (methane) conversion to metgas through bireforming (U.S. Pat. Nos. 7,906,559; 8,133,926; 8,440,729 and J. Am. Chem. Soc.
• Dry CO 2 fracking as stated eliminates environmental and safety problem caused by hydrofracking. Converting shale gas to liquid methanol through metgas makes it readily transportable and to be used as a transportation fuel for cars, modified diesel trucks and ships as well as a chemical raw material for derived products. The proposed method also mitigates the harmful effect of CO 2 emission into the atmosphere and eliminates contamination of subterranean water sources caused by hydrofracking significantly, “dry CO 2 fracking” followed by methanol synthesis also provides a solid economic basis for the overall process.
• the present invention discloses a feasible and economic way to replace hydrofracking, which uses very large amounts of water and harmful chemicals with dry CO 2 gas fracking. It also allows ready liquefaction of produced shale gas to methanol for replacing oil as a convenient liquid transportation fuel and chemical source material.
• CCS carbon capture and sequestration
• the first step of the method involves injecting pressurized carbon dioxide from any source into the shale formation resulting in fracture and displacing the trapped gas and allowing it to be recovered through the borehole.
• the CO 2 gas pressure is generally between 10 to 100 atm, which can easily be attained with the use of conventional compressors, pumps and piping equipment. If needed, injection equipment can also be used to introduce with the dry CO 2 gas a solid particulate propping material such as sand (see, e.g., US patent application publication 2007/0000666). No chemical additives are needed as the pressurized injection of CO 2 alone is sufficient to achieve fracking.
• the bulk of the injected CO 2 is recovered from the produced shale gas and can be recycled for the fracking process. Part of it, however, can be retained in the extracted shale rock rendering it more stable and providing permanent safe sequestration.
• the liberated mixture of shale gas and used CO 2 after purifying it mainly to remove hydrogen sulfide and other impurities, is then adjusted with the addition of water (generally as steam) to obtain a mixture of methane, CO 2 and steam in 3:1:2 molar ratio to form the needed fuel for the bireforming step and subsequent methanol synthesis using a mixture of CO and hydrogen in 1:2 molar ratio.
• water generally as steam
• the purification steps are known and practiced in existing natural gas production.
• Hydrogen sulfide is removed to avoid also catalyst poisoning.
• the removed hydrogen sulfide can be converted to elemental sulfur or non-toxic sulfur compounds, which can be recovered or discarded (see for example, US patent application publication 2013/0216460).
• the birefoming step is described in US patent application publication 2012/0115965.
• the bireforming reaction is conducted by passing the gas mixture over a catalyst, such as the catalysts disclosed in the US patent publication, and at a temperature between about 800° C. and 1100° C., preferably from about 800° C.
• metgas namely a syn-gas mixture of carbon monoxide/hydrogen (CO/H 2 ) in a molar ratio of about 2:1, preferably between 2:1 and 2.1:1, and most preferably about 2.05:1; and subsequently further sufficient combination to convert such mixture of H 2 and CO exclusively to methanol, as follows: 3CH 4 +CO 2 +2H 2 O ⁇ 4CO+8H 2 which then results in the further transformation: 4CO+8H 2 ⁇ 4CH 3 OH.
• CO/H 2 carbon monoxide/hydrogen
• a catalyst or combination of catalysts are to be used.
• These catalysts include any suitable metal or metal oxide, including without limitation a metal such as V, Ti, Ga, Mg, Cu, Ni, Mo, Bi, Fe, Mn, Co, Nb, Zr, La or Sn, and corresponding oxides of such metals.
• These catalysts may be used as a single metal, or a combination of a metal and metal oxide, or a combination of metal oxides, supported on a suitable support such as a high surface area nanostructured oxide support such as fumed silica or fumed alumina.
• NiO, metal-metal oxides such as Ni—V 2 O 5 , M 2 O 3 —V 2 O 5 , and NiO—V 2 O 5 , as well as mixed oxides such as Ni 2 V 2 O 7 and Ni 3 V 2 O 8 can be used.
• the preferred catalysts include Cu/ZnO catalysts and the bireforming reaction is conducted at atmospheric pressure in a flow reactor at a temperature between 220 to 250° C.
• a number of other related metal and metal oxide catalysts, and their combinations, can also be used. Needed suitable reactors for the conversion reactions as well as pressurized continuous flow reactors are well known and commercially available.
• the necessary carbon dioxide for the dry fracking process can be obtained from any available natural or industrial sources such as carbon fuel burning power plants, chemical plants, cement plants, etc.
• the needed new infrastructure essentially involves only CO 2 pipelines from various industrial CO 2 producing sources or natural sources.
• the CO 2 used in the dry fracking is captured, separated and recycled. Some of the CO 2 as mentioned is utilized in the bireforming process.
• the only use of water in the overall process is the stoichiometric amount of steam needed in the bireforming unit for subsequent metgas synthesis. This eliminates the potential harmful environmental and geological effects of the use of water in hydrofracking.
• a further significant aspect of our invention is that the safely and efficiently prepared methanol from abundant shale gas sources using the disclosed process can be used to prepare methanol as the common fuel for all internal combustion engines (including modified diesel vehicles, maritime vessels, trains, military vehicles, etc.) replacing oil and its products.
• This eliminates presently needed separate infrastructures and transportation (storage) systems for gasoline and diesel fuel using vehicles.
• Advances in modified diesel engines developed recently at MIT K. Bullis, MIT Technology Review, Mar. 28, 2013
• methanol can also be readily converted into conventional hydrocarbon (including diesel) fuels and derived chemical products using the Exxon-Mobil zeolite of Olah et. al., supported bifunctional acid-base catalyst based systems (G. A. Olah and A. Molnar, “Hydrocarbon Chemistry”, 2 nd ed., 2004, Wiley and references therein) replacing petroleum oil and dependence on oil monopolies.
• the dry fracking of shale gas with pressurized CO 2 is carried out by injecting pressurized (10-100 atm) CO 2 through the borehole involving both vertical and horizontal sections for fracking the shale formation and releasing the liberated shale gas containing methane together with the added CO 2 .
• a shale gas (natural gas) CO 2 mixture obtained from CO 2 dry fracking process is purified from hydrogen sulfide, adjusted with addition of CO 2 and steam to obtain a molar ratio 3:1:2 of methane, CO 2 and steam, which upon reforming process in a flow reactor over a catalyst such as NiO at a temperature of about 800° C. to 1100° C., preferentially between 800-850° C. yields metgas.
• Suitable catalysts include other varied metal and metal oxides such as V, Ti, Ga, Mg, Cu, Ni, Mo, Bi, Fe, Mn, Co, Nb, Zr, or Sn used as single metal, metal oxides or their combination.
• a preferred catalyst is NiO on fused alumina support or a CU/ZnO catalyst. This process provides a mixture that only contains CO and H 2 .
• Hydrogen and carbon monoxide produced in approximately 2:1 ratio are converted to produce methanol under catalytic reaction conditions using usual copper and zinc oxides and related catalysts.
• Methanol produced in Example 3 is dehydrated to dimethyl ether using a solid acid catalyst such as Nafion H between 100° C. to 200° C.

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• 2014
  • 2014-11-14 CA CA2930135A patent/CA2930135C/fr active Active
  • 2014-11-14 US US15/036,506 patent/US10131599B2/en active Active
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